摘要
针对湍流搅拌槽内固液悬浮过程进行了颗粒解析的数值模拟:搅拌雷诺数Re=9800,固体颗粒处于部分悬浮状态。采用格子玻尔兹曼方法对液相流体进行直接数值模拟,并基于浸没边界法在颗粒尺度下解析固体颗粒的运动。为验证数值模拟结果,利用颗粒解析PIV实验获得了颗粒体积分数在1%~8%工况下液相平均速度场和湍流动能分布。结果表明,颗粒解析数值模拟结果与PIV实验数据吻合良好。本文模拟方法可为模化固液两相搅拌体系中固体颗粒间以及颗粒与液相流体间复杂相互作用提供一种新思路。
In this paper,a particle-resolved simulation of the solid-liquid suspension in a turbulent stirred tank was presented,where the stirring Reynolds number Re=9800 and the solid particles were in a partially suspended state.The lattice-Boltzmann method was employed to simulate the liquid phase flow directly and the motion of the solid particles was resolved at the particle scale based on the immersed boundary method.In order to validate the results of the numerical simulations,the particle-resolved PIV experiments were performed to investigate the average velocity fields and the distribution of turbulent kinetic energy of the liquid phase under the conditions with particle volume fractions ranging from 1%to 8%.The results demonstrated a good agreement between the particle-resolved simulations and the PIV experimental data.The simulation methodology presented in this paper could offer a novel perspective for modeling the complex interactions among the solid particles and between the particles and the liquid phase flow in the solid-liquid two-phase stirred systems.
作者
李庚鸿
李志鹏
高正明
DERKSEN Jos
LI Genghong;LI Zhipeng;GAO Zhengming;DERKSEN Jos(SINOPEC Research Institute of Petroleum Processing Co.,Ltd.,Beijing 100083,China;School of Chemical Engineering,Beijing University of Chemical Technology,Beijing 100029,China;School of Engineering,University of Aberdeen,Aberdeen AB243UE,UK)
出处
《化工进展》
北大核心
2025年第8期4567-4570,共4页
Chemical Industry and Engineering Progress
关键词
固液悬浮
搅拌槽
湍流
格子玻尔兹曼
颗粒解析模拟
solid-liquid suspension
stirred tank
turbulence
lattice-Boltzmann
particle-resolved simulation
